JPH06126105A - Organic sewage filtration method and apparatus - Google Patents

Organic sewage filtration method and apparatus

Info

Publication number
JPH06126105A
JPH06126105A JP30320692A JP30320692A JPH06126105A JP H06126105 A JPH06126105 A JP H06126105A JP 30320692 A JP30320692 A JP 30320692A JP 30320692 A JP30320692 A JP 30320692A JP H06126105 A JPH06126105 A JP H06126105A
Authority
JP
Japan
Prior art keywords
gas
tank
filled layer
filtration
blower
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP30320692A
Other languages
Japanese (ja)
Other versions
JP2572336B2 (en
Inventor
Katsuyuki Kataoka
克之 片岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Ebara Research Co Ltd
Original Assignee
Ebara Research Co Ltd
Ebara Infilco Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Research Co Ltd, Ebara Infilco Co Ltd filed Critical Ebara Research Co Ltd
Priority to JP30320692A priority Critical patent/JP2572336B2/en
Publication of JPH06126105A publication Critical patent/JPH06126105A/en
Application granted granted Critical
Publication of JP2572336B2 publication Critical patent/JP2572336B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To prevent propagation of malodor by sucking a gas from a space part in the upper part of a granular filtering material-filled layer and introducing the gas into the lower part of the filled layer and discharging water in the filled layer through the bottom part of a tank at the time of cleaning the granular filtering material-filled layer, regarding a filtration apparatus for sewage, etc. CONSTITUTION:A blower 8 is operated to suck a gas in the inside of the space B in the upper part of a filtration tank 1, the gas in jetted out of a gas jetting pipe 9 through a gas sucking pipeline 7 and owing to the rising movement of bubbles, a granular filtering material in a filled layer A is stirred, This operation is continued for a prescribed duration. During the time, the generated malodor is circulated only in the closed system and is not released outside. Then, while the blower 8 is kept operating, a valve 12 is opened and water in the filtration tank 1 is drained to the lower part grating. At that time, a valve 13 is opened and outside air is introduced through a gas introducing pipe 14 and the pressure of the tank 1 is prevented from becoming negative and discharging to the discharging pipe 5 is carried out smoothly.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、下水などの有機性汚水
のSSをろ過除去すると共に、ろ過層を洗浄する際に、
悪臭が放散されないようにした新規ろ過装置およびその
洗浄方法に関する。
BACKGROUND OF THE INVENTION The present invention is intended to remove SS of organic sewage such as sewage by filtration and to wash the filter layer.
The present invention relates to a novel filtration device and a method for cleaning the same, which prevent odors from being emitted.

【0002】[0002]

【従来の技術】下水中のSSを沈殿させてから生物処理
するプロセスが、従来から代表的であったが、沈殿法は
SSの除去率が悪く、SS分離速度も小さいという欠点
がある。最近、沈殿法に代えて下水を粒状の大きな粒状
ろ材(中空プラスチック粒状物など)を充填したろ過層
に供給して、SSをろ過除去する方法が試みられてい
る。(特開平2−17908号公報) このろ過装置は水面が大気解放であり、ろ過層を洗浄す
るのに、空気をブロワーによってろ過層の下部に送り込
んで、空気泡の上昇運動によって粒状ろ材を攪拌しなが
ら、ろ過層内の水を全量排水するという方法が採用され
ている。
2. Description of the Related Art Conventionally, a process of precipitating SS in sewage and then biologically treating it has been typical, but the precipitation method has drawbacks such as a low removal rate of SS and a low SS separation rate. Recently, instead of the precipitation method, a method has been attempted in which sewage is supplied to a filtration layer filled with a large granular filter material (hollow plastic granular material, etc.) to remove SS. (Japanese Patent Application Laid-Open No. 2-17908) In this filtration device, the water surface is open to the atmosphere, and in order to wash the filtration layer, air is sent to the lower part of the filtration layer by a blower, and the granular filter medium is agitated by the upward movement of air bubbles. However, the method of draining all the water in the filtration layer is adopted.

【0003】本発明者が、前記特開平2−17908号
公報に記されている技術を下水の処理を目的として追試
したところ、粒状ろ材を充填したろ過層内には多量の有
機性SSが捕捉されていて、前記ろ過層を空気で洗浄す
る時、H2 S、メルカプタン、アンモニアなどの悪臭が
激しく外部に揮散してくることが判明した。この現象
は、水温の高い夏期に特に激しかった。
When the present inventor re-tested the technique described in the above-mentioned Japanese Patent Application Laid-Open No. 2-17908 for the purpose of treating sewage, a large amount of organic SS was captured in the filtration layer filled with the granular filter medium. However, it was found that when the filter layer was washed with air, a bad odor of H 2 S, mercaptan, ammonia, etc. was violently emitted to the outside. This phenomenon was particularly severe during the summer when the water temperature was high.

【0004】[0004]

【発明が解決しようとする課題】本発明は従来のろ過装
置洗浄時の悪臭発生トラブルを効果的に解決することを
課題としたものである。1つの方法としては、ろ過層の
空気洗浄(以下空洗と略記する)時に排出される悪臭を
別個に設けた脱臭装置に導いて脱臭することが当然考え
られるが、そのための脱臭装置、送風機、管路など高額
な設備が必要になってくるという欠点がある。本発明
は、このような方法によらず、極めて効果的に悪臭発生
トラブルを防止することを課題とする。
SUMMARY OF THE INVENTION An object of the present invention is to effectively solve the trouble of generating an offensive odor during washing of a conventional filtration device. As one method, it is naturally conceivable to introduce a bad odor discharged at the time of air-cleaning the filter layer (hereinafter abbreviated as “air-cleaning”) to a separately provided deodorizing device for deodorizing. It has the drawback that expensive equipment such as pipelines is required. An object of the present invention is to very effectively prevent a trouble of generating an offensive odor regardless of such a method.

【0005】[0005]

【課題を解決するための手段】上記課題は、以下に述べ
る本発明の手段によって効果的に解決される。すなわ
ち、 (1)槽内に設けた粒状ろ材充填層に汚水を通過させる
有機性汚水のろ過方法において、粒状ろ材充填層の洗浄
時に、該充填層上方に密閉可能に設けた空間部よりガス
を吸引し、該充填層下部に導入すると共に、該槽底部よ
り充填層内の水を排水して充填層の洗浄を行うことを特
徴とする有機性汚水のろ過方法。 (2)槽内水面下に粒状ろ材充填層を設け、水面上に外
気導入可能な密閉空間部を設け、該空間部からガスを吸
引し該充填層の下部に空間部からのガスを吐出させる流
路とガス吐出管を設け、該流路に送風機を配備すると共
に、該槽底部に排水部を設けたことを特徴とする有機性
汚水のろ過装置。である。
The above-mentioned problems can be effectively solved by the means of the present invention described below. That is, (1) in a method of filtering organic sewage in which sewage is passed through a granular filter medium packed layer provided in a tank, at the time of washing the granular filter medium packed layer, gas is introduced from a space portion provided above the packed layer in a sealable manner. A method for filtering organic sewage, which comprises suctioning and introducing into the lower part of the packed bed, and draining water in the packed bed from the bottom of the tank to wash the packed bed. (2) A granular filter medium filling layer is provided below the water surface in the tank, a closed space portion capable of introducing outside air is provided above the water surface, gas is sucked from the space portion, and gas from the space portion is discharged below the filling layer. An apparatus for filtering organic wastewater, comprising a flow passage and a gas discharge pipe, a blower provided in the flow passage, and a drainage portion provided at the bottom of the tank. Is.

【0006】(構成)以下に図1を用いて本発明の構成
の1例について説明する。ただし、本発明は以下の例に
制限されるものではない。図1において、1はろ過槽で
あり、槽1内には粒状ろ材を充填した充填層Aを有す
る。粒状ろ材としては空洗時に容易に攪乱される程度の
比重を有するものが好ましく、その材質、形状、粒径に
ついては被処理汚水の性状により適宜選定される。例え
ば、下水などに好ましいものとしては、粒径10〜30
mmの中空プラスチック製のろ材を用いることができ
る。
(Structure) An example of the structure of the present invention will be described below with reference to FIG. However, the present invention is not limited to the following examples. In FIG. 1, 1 is a filtration tank, and the tank 1 has a packed bed A filled with a granular filter medium. As the granular filter medium, one having a specific gravity that is easily disturbed during washing with air is preferable, and its material, shape and particle size are appropriately selected depending on the properties of the sewage to be treated. For example, a preferable particle size for sewage is 10-30
A hollow plastic filter material having a diameter of mm can be used.

【0007】槽1内の充填層Aの下方には有機性汚水の
流入部2を有し、層Aの上方にはろ過水流出部3を有し
ており、このろ過水流出部3の位置によって槽1の水面
4が決まる。槽1の水面4の上部には、カバー6をもっ
た密閉可能な空間Bが設けられ、空間Bはガス吸引管路
7を経てブロワー(送風機)8に連結され、さらにガス
吸引管路をと通って槽1内にガスを吹き込むガス吐出管
9に連結されている。充填層Aの上部と下部にはそれぞ
れ粒状ろ材の流出を防止する上部多孔性部材(グレーチ
ング)10および下部多孔性部材11が張設されてい
る。槽の底部には弁12を有する排水部5が、槽の最上
部(カバー6)には空間部B内へ外気を流入できるよう
弁13を有するガス流入管14が設けられている。この
ガス流入管14は本発明のろ過方法において重要な役割
を果たす管である。空間Bの高さは、ブロワー8の起動
時に水がガス吸引管路7に侵入しない程度であれば良
く、特にその高さは限定しない。
An inflow portion 2 of organic waste water is provided below the packed bed A in the tank 1, and a filtered water outflow portion 3 is provided above the bed A. The position of the filtered water outflow portion 3 is provided. The water surface 4 of the tank 1 is determined by this. A watertight space B having a cover 6 is provided above the water surface 4 of the tank 1, and the space B is connected to a blower (blower) 8 via a gas suction pipe line 7 and a gas suction pipe line. It is connected to a gas discharge pipe 9 through which gas is blown into the tank 1. An upper porous member (grating) 10 and a lower porous member 11 which respectively prevent the outflow of the granular filter medium are stretched above and below the packed bed A. A drain portion 5 having a valve 12 is provided at the bottom of the tank, and a gas inflow pipe 14 having a valve 13 for allowing outside air to flow into the space B is provided at the top of the tank (cover 6). The gas inflow pipe 14 is a pipe that plays an important role in the filtration method of the present invention. The height of the space B may be such that water does not enter the gas suction conduit 7 when the blower 8 is started, and the height thereof is not particularly limited.

【0008】以上の構成よりなる本発明のろ過槽は、通
常ろ過処理のための運転時には散気を行うことなく、上
向流で汚水のろ過処理を行う。しかして、本発明のろ過
装置を運転して汚水のろ過を行うに伴って、有機性汚水
中のSSが充填層Aでろ過され、SSが30mg/リッ
トル以下のろ過水が得られるが、長時間ろ過を続けると
ろ過処理水中にSSが多量にリークするようになるの
で、この時点で有機性汚水の供給を停止し、次の作用で
述べる本発明独自の方法によって、悪臭の放散を防止し
つつ、充填層Aの洗浄を行う。
In the filtration tank of the present invention having the above-mentioned constitution, the wastewater is filtered by the upward flow without air diffusion during the operation for normal filtration. Then, as the filter device of the present invention is operated to filter the wastewater, SS in the organic wastewater is filtered in the packed bed A, and filtered water having SS of 30 mg / liter or less is obtained. Since a large amount of SS will leak into the filtered water when the filtration is continued for a long time, the supply of the organic wastewater is stopped at this point, and the emission of the malodor is prevented by the method unique to the present invention described in the following action. Meanwhile, the packed bed A is washed.

【0009】(作用)図1により本発明のろ過槽1の充
填層Aの洗浄法について説明する。 1)ブロワー8を駆動し、空間部B内のガスを吸引し、
そのガスを槽1内にガス吐出管9から噴出させ、気泡の
上昇運動によって充填層A内の粒状ろ材を激しく攪乱す
る。この操作を数分間続ける。この時充填層Aから悪臭
が放出されるが、ブロワー8によってガス吐出管9から
吐出されたガスは、充填層A内を上昇し、空間部Bに達
し、再びガス吸引管路7を通ってブロワー8に吸引され
循環するので、外部に悪臭がもれることはない。これが
本発明の要点の1つであり、従来、このようにガスを循
環させながらろ過層を洗浄するという例は存在しない。
(Operation) A method of cleaning the packed bed A of the filtration tank 1 of the present invention will be described with reference to FIG. 1) Drive the blower 8 to suck the gas in the space B,
The gas is ejected from the gas discharge pipe 9 into the tank 1, and the granular filter medium in the packed bed A is violently disturbed by the ascending movement of the bubbles. Continue this operation for a few minutes. At this time, a bad odor is released from the packed bed A, but the gas discharged from the gas discharge pipe 9 by the blower 8 rises in the packed bed A, reaches the space B, and passes through the gas suction conduit 7 again. Since it is sucked into the blower 8 and circulated, no bad odor is leaked to the outside. This is one of the main points of the present invention, and conventionally, there is no example of cleaning the filtration layer while circulating the gas in this way.

【0010】2)ブロワー8を駆動したまま、弁12を
開き、ろ過槽内の水を下部グレーチング11までドレー
ンすると、充填層A内に捕捉されていたSSが槽外に排
出される。この操作で重要な役割を果たすのが、外気導
入路14である。もしも、外気導入路14が存在しない
と、弁13を開けても槽内が負圧になり、全く排水でき
ないので、充填層Aを洗浄できない。ブロワー8を駆動
しながら、弁13を解放すると、ろ過槽内の水が排水さ
れるが、その排水量に等しい容積の外気が外気導入路1
4から槽1内に流入するので、槽1内が負圧になること
はなく、排水部5の管路からスムーズな排水が可能にな
る。ドレーンは急速に行うことが好ましい。しかして排
水が終了した後、ブロワー8を止め、弁12を閉じて操
作2)を終了する。
2) While the blower 8 is still driven, the valve 12 is opened and the water in the filtration tank is drained to the lower grating 11 to discharge the SS trapped in the packed bed A out of the tank. The outside air introduction passage 14 plays an important role in this operation. If the outside air introducing passage 14 does not exist, even if the valve 13 is opened, the inside of the tank will have a negative pressure, and drainage cannot be performed at all, so that the packed bed A cannot be washed. When the valve 13 is opened while driving the blower 8, the water in the filtration tank is drained, but the outside air having a volume equal to the amount of the drained water is introduced into the outside air introduction passage 1
Since it flows into the tank 1 from 4, the inside of the tank 1 does not become a negative pressure, and smooth drainage is possible from the pipeline of the drainage section 5. It is preferable that the drainage be performed rapidly. Then, after the drainage is completed, the blower 8 is stopped, the valve 12 is closed, and the operation 2) is completed.

【0011】以上で充填層Aの洗浄を、悪臭を外部に放
出させることなく行うことができる。なお、外気導入路
14を密閉カバー部6に設けずに、ろ過水流出部3を外
気導入路の役割と兼用しても良い。すなわち、弁12を
開け排水すると、ろ過水流出路3を通って外気が流入で
きるよう構成しても良い。しかして、再び有機性汚水2
を供給して、ろ過処理を再開すると、槽1内水位が少し
ずつ上昇し、それにつれて槽1内のガスが少しずつ外気
導入路14を通って外に排出されてゆくが、その量は少
量であるので、いかようにでも容易に処分できる。例え
ば、本発明のろ過工程の後工程には、活性汚泥処理など
の生物処理施設を通常設けるが、この活性汚泥処理のエ
アレーションを行うブロワー室に前述の少量の悪臭ガス
を導き大量の空気と共に、エアレーションタンクに送り
込んで生物脱臭するのが合理的である。
As described above, the filling layer A can be washed without releasing a bad odor to the outside. The filtered water outflow portion 3 may also serve as the outside air introduction passage without providing the outside air introduction passage 14 in the closed cover portion 6. That is, when the valve 12 is opened and drained, outside air may flow in through the filtered water outflow passage 3. Then, again organic sewage 2
When water is supplied and the filtration process is restarted, the water level in the tank 1 rises little by little, and the gas in the tank 1 is gradually discharged to the outside through the outside air introduction passage 14, but the amount is small. Therefore, it can be easily disposed of in any way. For example, in the subsequent step of the filtration step of the present invention, a biological treatment facility such as activated sludge treatment is usually provided, but with a large amount of air by introducing a small amount of the aforementioned malodorous gas into a blower chamber that performs aeration of this activated sludge treatment, It is rational to send it to the aeration tank to deodorize the organisms.

【0012】[0012]

【発明の効果】【The invention's effect】

(1)有機性汚水中の有機性SSを効果的にろ過除去す
ることができ、ろ過層を洗浄する際にも悪臭が外部に拡
散しない。従って、特別な脱臭設備が不要であり、極め
て合理的である。 (2)悪臭が外部に拡散しないので、ろ過層を充分なガ
ス量で洗浄できる。(従来は、空気でろ過層を洗浄する
ので、洗浄空気使用量と同じ量の悪臭ガスが系外に排出
されてしまうという欠点があった。)
(1) The organic SS in the organic wastewater can be effectively removed by filtration, and the odor does not diffuse to the outside even when the filtration layer is washed. Therefore, no special deodorizing equipment is required, which is extremely rational. (2) Since the malodor does not diffuse to the outside, the filtration layer can be washed with a sufficient amount of gas. (In the past, since the filter layer was washed with air, there was a drawback that the same amount of malodorous gas as the amount of washing air used was discharged outside the system.)

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明のろ過装置の作用を示す装置の断面説明
FIG. 1 is an explanatory sectional view of a device showing the operation of the filtration device of the present invention.

【符号の説明】[Explanation of symbols]

1 ろ過槽 2 有機性汚水流入部 3 ろ過水流出部 4 槽内水面 5 排水部 6 カバー 7 ガス吸引管路 8 ブロワー 9 ガス吐出管 10 上部多孔性部材 11 下部多孔性部材 12 弁 13 弁 14 ガス流入管 A 充填層 B 空間部 1 Filter Tank 2 Organic Sewage Inflow Portion 3 Filtered Water Outflow Portion 4 Tank Internal Water Surface 5 Drainage Portion 6 Cover 7 Gas Suction Pipeline 8 Blower 9 Gas Discharge Pipe 10 Upper Porous Member 11 Lower Porous Member 12 Valve 13 Valve 14 Gas Inflow pipe A Packed bed B Space

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 8925−4D B01D 29/08 Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location 8925-4D B01D 29/08 Z

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 槽内に設けた粒状ろ材充填層に汚水を通
過させる有機性汚水のろ過方法において、粒状ろ材充填
層の洗浄時に、該充填層上方に密閉可能に設けた空間部
よりガスを吸引し、該充填層下部に導入すると共に、該
槽底部より充填層内の水を排水して充填層の洗浄を行う
ことを特徴とする有機性汚水のろ過方法。
1. A method for filtering organic sewage in which sewage is allowed to pass through a granular filter medium packed layer provided in a tank, wherein a gas is introduced from a space that is hermetically sealed above the granular filter medium packed layer when the granular filter medium packed layer is washed. A method for filtering organic sewage, which comprises suctioning and introducing into the lower part of the packed bed, and draining water in the packed bed from the bottom of the tank to wash the packed bed.
【請求項2】 槽内水面下に粒状ろ材充填層を設け、水
面上に外気導入可能な密閉空間部を設け、該空間部から
ガスを吸引し該充填層の下部に空間部からのガスを吐出
させる流路とガス吐出管を設け、該流路に送風機を配備
すると共に、該槽底部に排水部を設けたことを特徴とす
る有機性汚水のろ過装置。
2. A granular filter medium filling layer is provided below the water surface in the tank, and a closed space portion capable of introducing outside air is provided above the water surface. Gas is sucked from the space portion and gas from the space portion is provided below the filling layer. A filter device for organic wastewater, comprising a flow passage for discharging and a gas discharge pipe, a blower provided in the flow passage, and a drainage portion provided at the bottom of the tank.
JP30320692A 1992-10-16 1992-10-16 Organic wastewater filtration method and apparatus Expired - Lifetime JP2572336B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30320692A JP2572336B2 (en) 1992-10-16 1992-10-16 Organic wastewater filtration method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30320692A JP2572336B2 (en) 1992-10-16 1992-10-16 Organic wastewater filtration method and apparatus

Publications (2)

Publication Number Publication Date
JPH06126105A true JPH06126105A (en) 1994-05-10
JP2572336B2 JP2572336B2 (en) 1997-01-16

Family

ID=17918162

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30320692A Expired - Lifetime JP2572336B2 (en) 1992-10-16 1992-10-16 Organic wastewater filtration method and apparatus

Country Status (1)

Country Link
JP (1) JP2572336B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009291725A (en) * 2008-06-06 2009-12-17 N Ii T Kk Sewage treatment apparatus
JP2013248563A (en) * 2012-05-31 2013-12-12 Kamata Bio Eng Kk Filtering device, filtering method of the same, and backwashing method of filter medium

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009291725A (en) * 2008-06-06 2009-12-17 N Ii T Kk Sewage treatment apparatus
JP2013248563A (en) * 2012-05-31 2013-12-12 Kamata Bio Eng Kk Filtering device, filtering method of the same, and backwashing method of filter medium

Also Published As

Publication number Publication date
JP2572336B2 (en) 1997-01-16

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